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WO2018195789A1 - Method and burner for heating a furnace for metal processing - Google Patents

Method and burner for heating a furnace for metal processing Download PDF

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Publication number
WO2018195789A1
WO2018195789A1 PCT/CN2017/081959 CN2017081959W WO2018195789A1 WO 2018195789 A1 WO2018195789 A1 WO 2018195789A1 CN 2017081959 W CN2017081959 W CN 2017081959W WO 2018195789 A1 WO2018195789 A1 WO 2018195789A1
Authority
WO
WIPO (PCT)
Prior art keywords
fuel
supply line
furnace
central
flow
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/CN2017/081959
Other languages
English (en)
French (fr)
Inventor
Martin Adendorff
Joachim Von Scheele
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Linde GmbH
Original Assignee
Linde GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to RU2019133630A priority Critical patent/RU2733614C1/ru
Priority to KR1020197034656A priority patent/KR102429928B1/ko
Priority to UAA201910551A priority patent/UA124285C2/uk
Priority to US16/607,869 priority patent/US11852336B2/en
Priority to EP17908004.9A priority patent/EP3615699A4/en
Priority to MYPI2019006239A priority patent/MY197759A/en
Priority to CA3059799A priority patent/CA3059799C/en
Priority to CN201780090039.9A priority patent/CN110603335B/zh
Application filed by Linde GmbH filed Critical Linde GmbH
Priority to PCT/CN2017/081959 priority patent/WO2018195789A1/en
Priority to BR112019021862-9A priority patent/BR112019021862B1/pt
Publication of WO2018195789A1 publication Critical patent/WO2018195789A1/en
Priority to ZA2019/07070A priority patent/ZA201907070B/en
Anticipated expiration legal-status Critical
Priority to US18/389,344 priority patent/US20240077200A1/en
Ceased legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/20—Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone
    • F23D14/22—Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone with separate air and gas feed ducts, e.g. with ducts running parallel or crossing each other
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/52—Manufacture of steel in electric furnaces
    • C21C5/5211—Manufacture of steel in electric furnaces in an alternating current [AC] electric arc furnace
    • C21C5/5217—Manufacture of steel in electric furnaces in an alternating current [AC] electric arc furnace equipped with burners or devices for injecting gas, i.e. oxygen, or pulverulent materials into the furnace
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/0075—Treating in a ladle furnace, e.g. up-/reheating of molten steel within the ladle
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/74—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
    • C21D1/76—Adjusting the composition of the atmosphere
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C1/00—Combustion apparatus specially adapted for combustion of two or more kinds of fuel simultaneously or alternately, at least one kind of fuel being either a fluid fuel or a solid fuel suspended in a carrier gas or air
    • F23C1/12—Combustion apparatus specially adapted for combustion of two or more kinds of fuel simultaneously or alternately, at least one kind of fuel being either a fluid fuel or a solid fuel suspended in a carrier gas or air gaseous and pulverulent fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/32—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid using a mixture of gaseous fuel and pure oxygen or oxygen-enriched air
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/46—Details
    • F23D14/48—Nozzles
    • F23D14/58—Nozzles characterised by the shape or arrangement of the outlet or outlets from the nozzle, e.g. of annular configuration
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D3/00—Charging; Discharging; Manipulation of charge
    • F27D3/16—Introducing a fluid jet or current into the charge
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D99/00—Subject matter not provided for in other groups of this subclass
    • F27D99/0001—Heating elements or systems
    • F27D99/0033—Heating elements or systems using burners
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D2900/00—Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
    • F23D2900/21—Burners specially adapted for a particular use
    • F23D2900/21001—Burners specially adapted for a particular use for use in blast furnaces
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/20—Recycling
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/32—Technologies related to metal processing using renewable energy sources

Definitions

  • the present invention relates to a method and a burner for heating a furnace for metal processing by combusting a fuel in the furnace by supplying an oxidizing gas through an oxidizing gas supply line into the furnace and by supplying a fuel through a fuel supply line into the furnace.
  • LTOF low-temperature oxy-fuel combustion technology
  • the combustion occurs under a diluted oxygen concentration by mixing the furnace gases into the combustion zone. This results in lower flame temperatures, below the point at which thermal NOx is created. Further, the energy is dispersed throughout the entire furnace for uniform heating and more efficient melting. Typical benefits are a higher melt rate of up to 50%, up to 50%lower fuel combustion, the avoidance of hotspots in the furnace, reduced flue gas volumes and NOx emissions.
  • the flameless and semi flameless burner technologies all rely on the very high velocity oxygen jets to generate the flameless effect.
  • the oxygen outlet velocity is typically the speed of sound in oxygen, around 305 m/s. Velocities from about 100 m/supwards can also be used.
  • the high velocity jets create a very strong recirculation within the furnace gas space, resulting in the above mentioned reduced NOx generation by reducing peak temperatures within the flame and in a very homogeneous heating of the furnace.
  • Such burner technologies have proven very efficient and useful especially in essentially clean dust free furnace atmospheres.
  • a shrouded injector comprises an inner pipe through which oxygen enriched air is injected.
  • the inner pipe is surrounded by an annulus through which nitrogen (or other inert gases or hydrocarbon) flows.
  • nitrogen or other inert gases or hydrocarbon
  • the pressures at which the gases are injected prevent the accretion from blocking the flow of gas, so the shrouded injector operates without a need for punching.
  • the ALSI technology is, however, not a burner technology, but makes use of an air/oxygen injection system that is used under a liquid copper or nickel bath. The intention is to move the very hot exothermic reactions away from the tuyere tip in order to prevent them from being damaged by the high heat generation.
  • the benefits of known flameless and semi flameless burner technologies namely, a reduced NOx generation and homogeneous heating of the furnace, should be retained as far as possible.
  • the present invention provides a method for heating a furnace used for metal processing by combusting a fuel in the furnace by supplying an oxidizing gas through an oxidizing gas supply line into the furnace and by supplying a fuel through a fuel supply line into the furnace and a corresponding burner having at least one oxidizing gas supply line and at least one fuel supply line according to the independent claims.
  • Advantageous embodiments are the subject matter of the dependent claims and the description that follows.
  • the oxidizing gas is supplied in form of a central oxidizing gas flow together with a first shroud gas flow and/or the fuel is supplied in form of a central fuel flow together with a second shroud gas flow.
  • the corresponding burner according to the present invention has at least one oxidizing gas supply line comprising a central oxidizing supply line for suppling oxidizing gas and a first annular supply line surrounding the central oxidizing gas supply line for supplying a first shroud gas flow and/or at least one fuel supply line comprising a central fuel supply line for supplying fuel and a second supply line surrounding the central fuel supply line for supplying a second shroud gas flow.
  • the ALSI technology as discussed above applies a shrouded submerged injection system which requires a second high pressure gas source, typically nitrogen. Oxygen cannot be used as a shroud gas because this would negate the object of moving the reaction zone away from the tuyere outlet.
  • a second high pressure gas source typically nitrogen.
  • Oxygen cannot be used as a shroud gas because this would negate the object of moving the reaction zone away from the tuyere outlet.
  • the central oxidizing gas flow it is preferred to use the same oxidizing gas as the first shroud gas flow.
  • the central gas (provided that the central flow is in form of a gas) is also used as the shroud gas. This simplifies the installation as less piping and control equipment is required.
  • the shroud gas proportion can be a pure mechanical function not prone to failure or control inaccuracies.
  • the velocity of the central oxidizing gas flow is higher than the velocity of the first shroud gas flow, especially the velocity of the central oxidizing gas flow is essentially or exactly equal to or even higher than the sonic velocity of the oxidizing gas. This enhances the suction effect whereby the first shroud gas flow is sucked into the central oxidizing gas flow.
  • fuel gases are typically supplied with a low supply pressure.
  • gaseous fuel like natural gas (NG) or LPG which can be supplied with a high enough supply pressure.
  • the ratio of the flow rates of the first shroud gas flow and the central oxidizing gas flow is adjusted.
  • the first annular supply line of the burner In order to implement an adjustment or a variation of the ratios of the respective flow rates it is preferred for the first annular supply line of the burner to be in fluid connection with at least two first nozzles opening up into the first annular supply line and/or for the second annular supply line to be in fluid connection with at least two second nozzles opening up into the second annular supply line.
  • the ratio of the flow rates of the shroud gas and central fluid flow can be varied according to the needs of the process.
  • a larger number of smaller nozzles is preferred to a single or fewer slightly larger nozzles. This is especially true if – especially in case of the oxidizing gas –the shroud gas is the same as the central fluid.
  • the same gas could be supplied to the central supply line and to the annular supply line.
  • a large number of smaller nozzles can prevent damage to the annular supply line material by the high velocity, especially sonic velocity, entering the narrow annulus. Too small holes would be susceptible to blocking by dirt entrained in the gas flow.
  • the first shroud gas flow is or contains the oxidizing gas and/or if the second shroud gas flow is or contains the fuel.
  • the shroud gas does not necessarily have to be the same as the central fluid.
  • the first shroud gas flow may be or may contain air, steam or flue gases (theoretically also an inert gas like argon, although it may not make economic sense, nitrogen should not be used as this will (may) increase NOx generation) or a combination thereof.
  • Such shroud gases would have to be supplied through at least one separate line, ideally also with some form of flow control or regulation .
  • the shroud gas could also be flue gases provided that the flue gases are sufficiently clean to avoid blocking of the nozzles and/or the annular supply line.
  • the nozzles are used to create a fixed ratio (mechanically) between central and shroud flows when the same gas for the shroud as for the central flow is used. If one uses a different shroud gas, then there will be no such connection between the central gas and the shroud gas.
  • flue gases would have to be purified before using them as a shroud gas. Theoretically, one could use flue gases, but it may not be technically or economically feasible. If flue gases are used, then they would have to be cleaned to remove at least particles.
  • the second shroud gas flow may be or may contain air, steam or inert gas like nitrogen, argon or a combination thereof. It is noted that the fuel outlet could be implemented without any shrouding flow if the fuel outlet velocity is low, typically in the region of 80 to 100 m/s.
  • the fuel may be a gaseous fuel but also liquid fuels can be used for the present invention.
  • the recirculation of poorly atomised liquid fuel droplets is a potential concern especially for flameless oxy-fuel burners as these poorly atomized liquid fuel droplets get deposited on the refractory face surrounding the burner/the respective supply lines.
  • the shrouding of the liquid fuel can assist with the atomisation and reduce the likelihood of fuel being deposited on the surrounding refractory walls.
  • the oxidizing gas may be oxygen, especially customary oxygen of high pureness or air, especially when a high enough air pressure is available.
  • the invention can also be implemented for air-fuel burners and is not limited to oxy-fuel burners.
  • Fig. 1 schematically shows an oxidizing gas supply line or a fuel supply line of a burner according to an embodiment of the present invention
  • Fig. 2 shows the supply line of Fig. 1 in combination with a furnace used for metal processing implementing a method according to the present invention.
  • Fig. 1 schematically shows one of the oxidizing gas supply lines 20 of a burner 10 for heating an aluminum recycling furnace 40.
  • accretions were deposited around the burner oxygen nozzles/supply lines (this could also apply to the fuel supply, although it is more common on oxygen lines because of the much higher jet velocity) , usually the deposited material being fine dross dust and/or coarse solid particles –they could also be recirculated liquid metal droplets that deposit and then potentially solidify around the nozzle outlet.
  • the invention came about in trying to prevent the recirculation of liquid copper and slag droplets in a Peirce Smith converter that occurs during the air blowing phase .
  • Such accretions build up around the oxygen supply line 20 on the wall of the refractory 50. With a burner 10 comprising supply lines as shown in Figure 1 such accretions are largely reduced.
  • FIG. 1 shows one of the two oxygen supply lines 20 in a flameless oxy-fuel burner, e.g. of 1500 kW.
  • the oxygen supply lines or lances would normally (but must not) be identical in layout.
  • the burner 10 would typically require one fuel, e.g. natural gas, and two oxygen supply lines, with the oxygen supply lines typically installed in a single plane on either side of the central fuel supply line, the oxygen supply lines being around 50 mm away from the fuel supply line (outer wall to outer wall) .
  • This geometry is only exemplary and not relevant to the present invention.
  • the fuel supply line (30) may look similar to the oxygen supply line 20, but typically would have larger dimensions.
  • Figure 1 shows either an oxidizing gas supply line 20 or a fuel supply line 30.
  • the fuel supply line 30 would also have a central fuel supply line 31 and a second annular supply line 32.
  • the corresponding gas flows are labeled 34 and 35, respectively. It should be noted, however, that since the fuel is typically injected at lower velocities, either a reduced shroud flow 35 or no shroud flow 35 could be used. Therefore, in the following, for easy of illustration, only the oxidizing gas supply line 20 is described in further detail.
  • the sizing of this oxygen supply line 20 is for approximately 160 Nm3/h of oxygen at a 2 barg supply pressure, by using 3 x 3 mm nozzles 23 opening up into the outer annular supply line 25, an oxygen flow/first shroud gas flow 25 of around 35 Nm3/h will pass through into the annulus 25 exiting the outer annulus at around 25 m/s.
  • the balance of the oxygen flow 24 exits through the central supply line 21 preferably at the sonic velocity of oxygen. In this example, between 20 and 25%of the oxygen exits through the annulus 22. The dirtier the furnace environment, the higher this ratio would be.
  • the total fuel (NG) and oxygen flow must always correspond to what is required for the combustion process stoichiometry calculations.
  • the fuel gas is not injected at sonic velocity, although this is an option if sufficient pressure is available and if all safety standards and norms are complied with. If the fuel outlet velocity is low enough, then either a reduced shroud flow or no shroud flow could be used.
  • the ratio of shroud gas 25, 35 and central gas 24, 25 can be varied, according to the needs of the process.
  • a large number of smaller nozzles, especially in case of oxidizing gas supplying nozzles 23, are preferable to a single or fewer slightly larger nozzles.
  • the supply pipe feeding the oxidizing gas supply line 20 or the fuel supply line 30 is labeled 60.
  • FIG 2 shows schematically the part of the burner 10 of Figure 1 in e.g. an aluminum recycling furnace 40.
  • Oxygen is used as the oxidizing gas which is supplied with high pressure through the central oxygen supply line 21 and exits the supply line 21 in form of a high velocity jet 24.
  • oxygen is also used as the shroud gas. This simplifies the installation since less piping and controlling equipment is required.
  • the shroud gas proportion is a mechanical function depending on the pressure and the geometry and number of nozzles 23.
  • Oxygen exits the annulus 22 in form of an annular oxygen flow 25 as shown in Figure 2.
  • the high velocity central oxygen jet 24 sucks parts of the furnace atmosphere back into itself resulting in a recirculation of furnace gases 41.
  • the high velocity central jet 24 initially sucks the shrouding oxygen gas flow 25 into itself rather then the surrounding furnace atmosphere. Only once the shroud gas 25 has been aspired into the jet 24, the jet 24 will start sucking the furnace gases 41 into itself. The point of recirculation is thus moved away from the wall of the refractory 50 and away from the supply line tip. This reduces or even eliminates the deposition of solid or liquid particles in the recirculated furnace atmosphere around the supply line outlet on to the wall of the refractory 50.
  • the shroud gas must not necessarily be the same as the central gas.
  • the system is not limited to a single fuel and two to or four oxygen supply lines configuration.
  • a single oxygen supply line as well multiple oxygen supply lines (3, 5, 6 even 8) are also conceivable.
  • the system can also be implemented in air-fuel burners especially when a high enough air pressure is available.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Metallurgy (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Furnace Details (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Tunnel Furnaces (AREA)
PCT/CN2017/081959 2017-04-26 2017-04-26 Method and burner for heating a furnace for metal processing Ceased WO2018195789A1 (en)

Priority Applications (12)

Application Number Priority Date Filing Date Title
CA3059799A CA3059799C (en) 2017-04-26 Method and burner for heating a furnace for metal processing
UAA201910551A UA124285C2 (uk) 2017-04-26 2017-04-26 Спосіб та пальник для нагрівання печі для обробки металу
US16/607,869 US11852336B2 (en) 2017-04-26 2017-04-26 Method and burner for heating a furnace for metal processing
EP17908004.9A EP3615699A4 (en) 2017-04-26 2017-04-26 PROCESS AND BURNER FOR HEATING A METAL PROCESSING OVEN
MYPI2019006239A MY197759A (en) 2017-04-26 2017-04-26 Method and burner for heating a furnace for metal processing
CN201780090039.9A CN110603335B (zh) 2017-04-26 2017-04-26 用于加热金属加工用的熔炉的方法和燃烧器
PCT/CN2017/081959 WO2018195789A1 (en) 2017-04-26 2017-04-26 Method and burner for heating a furnace for metal processing
RU2019133630A RU2733614C1 (ru) 2017-04-26 2017-04-26 Способ и горелка для нагрева печи для обработки металла
KR1020197034656A KR102429928B1 (ko) 2017-04-26 2017-04-26 금속 가공용 노를 가열하기 위한 방법 및 버너
BR112019021862-9A BR112019021862B1 (pt) 2017-04-26 2017-04-26 Método e queimador para aquecer um forno para o processamento de metal
ZA2019/07070A ZA201907070B (en) 2017-04-26 2019-10-25 Method and burner for heating a furnace for metal processing
US18/389,344 US20240077200A1 (en) 2017-04-26 2023-11-14 Method and burner for heating a furnace for metal processing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2017/081959 WO2018195789A1 (en) 2017-04-26 2017-04-26 Method and burner for heating a furnace for metal processing

Related Child Applications (2)

Application Number Title Priority Date Filing Date
US16/607,869 A-371-Of-International US11852336B2 (en) 2017-04-26 2017-04-26 Method and burner for heating a furnace for metal processing
US18/389,344 Continuation US20240077200A1 (en) 2017-04-26 2023-11-14 Method and burner for heating a furnace for metal processing

Publications (1)

Publication Number Publication Date
WO2018195789A1 true WO2018195789A1 (en) 2018-11-01

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PCT/CN2017/081959 Ceased WO2018195789A1 (en) 2017-04-26 2017-04-26 Method and burner for heating a furnace for metal processing

Country Status (10)

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US (2) US11852336B2 (ru)
EP (1) EP3615699A4 (ru)
KR (1) KR102429928B1 (ru)
CN (1) CN110603335B (ru)
BR (1) BR112019021862B1 (ru)
MY (1) MY197759A (ru)
RU (1) RU2733614C1 (ru)
UA (1) UA124285C2 (ru)
WO (1) WO2018195789A1 (ru)
ZA (1) ZA201907070B (ru)

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UA124285C2 (uk) * 2017-04-26 2021-08-18 Лінде Акціенґезельшафт Спосіб та пальник для нагрівання печі для обробки металу
US11105502B2 (en) * 2019-06-17 2021-08-31 Honeywell International Inc. Staged fuel burner

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US11852336B2 (en) 2023-12-26
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BR112019021862A2 (pt) 2020-05-26
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